Anionic lactam catalyst system

ABSTRACT

IN THE BASE-CATALYZED SUBSTANTIALLY ANHYDROUS ANIONIC LACTAM POLYMERIZATION, THE IMPROVEMENT WICH COMPRISES DISSOLVING THE METAL LACTAM CATALYST IN AN N,N-DISUBSTITUTED, AMIDE OF THE FORMULA   R-CO-N(-R1)-R2   WHERE R IS HYDROGEN OR ANY MONOVALENT HYDROCARBON RADICAL, R1 AND R2 CAN BE ANY MNOVALENT HYDROCARBON RADICAL AND WHERE ANY TWO OF THE R&#39;&#39;S CAN BE JOINED TOGETHER TO FORM A HETEROCYCLIC RING, PRIOR TO ADDING SAID METAL LACTAM CATALYST TO THE MONOMERIC LACTAM TO BE POLYMERIZED. ALSO DESCRIBED IS A SOLUTION OF A METAL LACTAM IN THE N,N-DISUBSTITUTED AMIDES DESCRIBED ABOVE AS WELL AS A PROCESS FOR PREPARING THE SOLUTION COMPRISING REACTING THE METAL OR METAL COMPOUND WITH A LACTAM IN THE PRESENCE OF THE N,N-DISUBSTITUTED AMIDE.

United States Patent O 3,575,938 ANIONIC LACTAM CATALYST SYSTEM Paul A. Tierney, Ballwin, M0., assignor to Monsanto Company, St. Louis, M0.

N Drawing. Continuation-impart of application Ser. No. 565,076, July 14, 1966. This application Jan. 8, 1969, Ser. No. 789,946

Int. Cl. C08g 20/12 US. Cl. 26078 9 Claims ABSTRACT OF THE DISCLOSURE In the base-catalyzed substantially anhydrous anionic lactam polymerization, the improvement which comprises dissolving the metal lactam catalyst in an N,N-disubstituted amide of the formula where R is hydrogen or any monovalent hydrocarbon radical, R and R can be any monovalent hydrocarbon radical and where any two of the Rs can be joined together to form a heterocyclic ring, prior -to adding said metal lactam catalyst .-to the monomeric lactam to be polymerized. Also described is a solution of a metal lactam in the N,N-disubstituted amides described above as well as a process for preparing the solution comprising reacting the metal or metal compound with a lactam in the presence of the N,N-disubstituted amide.

CROSS REFERENCE TO RELATED APPLICATION This application is a continuation-in-part of copending patent application Ser. No. 565,076, filed July 14, 1966, now abandoned.

BACKGROUND OF THE INVENTION M MN H O C II II 0 O reactable lactam iminium substance monomer salt The iminium salt is the active catalyst of the lactam polymerization system. The patents mentioned above set forth several reactable substances which form iminium salts upon reaction with the lactam monomer as well as several iminium salts themselves. Some of the iminium salts suggested are the alkali metal lactams such as lithium, sodium and potassium lactams, the alkaline earth metal lactams such as magnesium, calcium, strontium and barium lactams, zinc lactam and aluminum lactam.

In any large volume process utilizing techniques described in the above patents, the efficient mixing of monomer, initiator, catalyst, and other additives prior to gela- Patented Apr. 20, 1971 ice tion of the system becomes of major importance. One method has been to mix together monomer, initiator and all other additives except catalyst, then add catalyst to the monomer system when polymerization is desired. When the initiated monomer is prepared in large batches, catalyzed, and immediately cast into relatively small molds which permits little or no mixing after casting, the catalyst is preferably added through some sort of mixing head. Failure to achieve adequate mixing results in longer polymerization times, incompletely polymerized products, low molecular weight polymer in the product and otherwise generally unsatisfactory compositions.

Recent developments in the area of anionic lactam polymerization permit the preparation of reinforced polylactam compositions having mechanical properties far superior to the unreinforced polylactam. The reinforcement is achieved through the adhesive bonding of organosilane-treated inorganic materials to the polylactam. Addition of suflicient inorganic to optimize the mechanical properties of the polymerized compositions, however, increases viscosity of the monomer slurry and makes mixing of catalyst and initiated monomer-inorganic slurry even more difficult. Further, some of the catalysts such as sodium lactam and magnesium lactam which provide reinforced polymeric compositions 'with the best mechanical properties can only be mixed with the monomer slurry with considerable diificulty because of their normally solid nature at room temperature. To achieve adequate mixing, the mixing head and all lines leading from the catalyst source must be heated in order to obtain a fluid material. At high temperatures, hydrolysis of the catalyst by trace amounts of water or initiation of the catalyst by trace amounts of carbon dioxide can lead to viscosity build-up and gelation of the catalyst stream in the mixing head or in the line leading to the head. Other catalyst precursors which react with lactam monomer to give an iminium salt can of course he used in place of the solid alkali metal or alkaline earth metal lactam. A Grignard reagent such as ethylmagnesium bromide is an example of such a material. The Grignard reagents, however, upon reaction with lactam monomer produce gaseous byproducts such as ethane in the case of ethylmagnesium bromide. The gaseous byproducts must be removed from the slurry prior to gelation to provide compositions with smooth void-free surfaces. Alkali metal hydrides are further examples of polymerization catalysts which provide polylactams with good mechanical properties, but which are quite diflicult to use in a large scale polymerization. Alkali metal hydrides such as sodium hydride are normally solid at room temperature and are so highly reactive at or near their melting point of 200 to 300 C. that their use in liquid form is intolerable. In addition, the metal hydrides, upon catalyzing a lactam polymerization, evolve a gaseous byproduct, hydrogen, which must be removed prior to gelation of the monomer.

A lactam polymerization catalyst system capable of overcoming the difficulties described above would be a welcome addition to the art. To alleviate or eliminate the above described problem, the catalyst system must be such that no gas evolution takes place upon addition of the catalyst to the monomer. The catalyst must, of course, induce a rapid polymerization producing a casting with good mechanical properties. In addition, the catalyst should be a liquid at or near room temperature, be reasonably stable to the effects of trace amounts of water and carbon dioxide while in the liquid condition and should have a reasonably long shelf life. Providing a catalyst system capable of performing in the above manner con stitutes the principal object of this invention. Another important object of this invention is the provision of a lactam polymerization using the catalyst system. Yet another object is the provision of a new process for preparing a solution of metal lactam with an unusually advantageous combination of properties. Additional ob jects, benefits and advantages will become apparent as the detail description of the invention proceeds.

SUMMARY OF THE INVENTION The improved catalyst system suggested for use in a base-catalyzed substantially anhydrous lactam polym erization comprises a metal lactam dissolved in an N,N- disubstituted amide of the formula Where R can be hydrogen or any monovalent hydrocarbon radical and where R and R can be any monovalent hydrocarbon radical and Where any two of the Rs can be joined together to form a heterocyclic ring. Particularly preferred catalyst solutions are those that are liquid at or near room temperature. The lower the temperature at which the catalyst solution can be maintained, the less likely it is to deteriorate and lose its activity. Hence, catalyst solutions Which are liquid at temperatures below 35 or 40 C. are particularly useful.

The metal lactam can be any metal lactam. Alkali metal lactams such as sodium or potassium lactam constitute one preferred group. Metal lactams containing metals less electropositive than the alkali metals can also be used even though their use results in lengthened polymerization times. Such metal lactams are particularly preferred for use herein when modified by reaction with a source of halogen as described in copending patent application Ser. No. 507,682, filed Nov. 15, 1965, now US. Pat. No. 3,451,963. Examples of such metal lactams include magnesium lactam and aluminum lactam. When the above catalyst components are reacted with a source of halogen, it is postulated that the resultant active catalyst has the where M is 'a metal, X is a halogen atom or atoms and R is an alkylene chain. The lactam component of the metal lactam can be any lactam. Oftentimes the lactam compo nent will be identical to the particular monomer being polymerized, but such a restriction is by no means essential. Concentrations of metal lactam are conveniently expressed in terms of millimoles per mole of monomer. Workable concentration can range from 0.1 millirnole per mole of monomer or less up to 200 millimoles per mole of monomer or more. If a source of halogen is used to modify the reactivity of the metal lactam catalyst, the teachings set forth in copending patent application Ser. No. 507,682, filed Nov. 15, 1965, can be used in conjunction with the examples set forth herein to provide acceptable catalyst systems.

The solvent for the catalyst is the most important feature of the present invention. Discovery of a suitable solvent for the lactam polymerization catalyst has made possible the elimination of one entire step from the casting process and has simplified the execution of several other steps in the process. In addition, the use of solvents described herein has facilitated the preparation of lactam polymerization catalyst of increased activity and storage stability. Solvents useable herein are the N,N-disubstituted amides having the formula set forth above. The R, R and R groups can be hydrocarbon groups of any size, but preferably have no more than 20 carbon atoms. Suitable groups include alkyl, alkenyl, alkynyl, aryl, alkaryl, aralkyl, and condenser ring aryl groups. Of course, the R, R and R groups can be further substituted with additional groups which do not interfere with a lactam polym- 4 erization such as amino and carbonyl groups. In addition, the R group in the above generic formula of suitable solvents can also be hydrogen. Examples of solvents include N,-N-dimethylformamide, -N,N-dimethylacetamide, N,N-dimethylpropionamide, N-phenyl, N-methyl acetamide, N-naphthyl-N-ethyl acetamide, N,N-diethyl isobutyramide, and N-methylformanilide, N-ethylacetanilide, N-ethyl-4-nitroacetanilide, N-n-butylacetanilide, N-methyl o acetotoluidide, N,N' p phenylenebisacetanilide, 2-chloro N ethylacetanilide, N,N-diphenylacetamide, N,N diphenylformamide, N,N diethylformamide, N- methyl-N-l-naphthylacetamide, N,N-di-n-butylacetamide, N,N-diisopropylpropionamide, N-butyl N octyldecanamide, N,-N-dimethylbenzamide, N,N diethyl p toluamide, N methylpyrrolidone, N octylpiperidone, N-phenyl caprolactam, and others. When the R and R groups are joined to form a heterocyclic ring as in N-methyl-a-pyrrolidone, the heterocyclic group preferably but not necessarily contains up to about 12 carbon atoms. Examples include N-ethyl-a-pyrrolidone, N-phenyl piperidone, N-isobutyl caprolactam and N-cyclohexyl dodecanolactam. When the R and R groups are joined to form a heterocyclic ring, the heterocyclic group preferably has either five or six carbon atoms. Examples include N-acetyl pyridine, N-acetyl piperidine, N-propionyl morpholine, and N-acetyl morpholine. As mentioned above, catalyst solutions which are liquid at temperatures below 35 or 40 C. are particularly preferred. Such solutions which are liquid at low temperatures can be prepared by selecting a solvent from the abovedescribed class which is itself a liquid at the low temperature. The melting points of such compounds can be easily ascertained from a number of references. Examples of solvents of the above class which are liquids at temperatures below 40 C. are N-methylpyrrolidone, N,N-dimethylacetamide, N-methylformanilide, N-n-butyl acetanilide, N,N-diethyl formamide, and -N-acetyl piperidine.

The relative proportions of solvent and active catalyst in the catalyst solution will vary depending upon a number of factors such as the solubility of one particular catalyst in one particular solvent, the temperature at which the catalyst solution will be metered into the monomer, and the ease with which the monomer and catalyst can be mixed together. In general, liquid solutions containing 50% or 75% or more by weight of active catalyst can be prepared especially if the solution can be maintained at some temperature above or C. Usually, solutions containing 25 or 30% by weight of sodium caprolactam or magnesium caprolactam in N-alkylpyrrolidones at room temperatures can be prepared. Of course, solutions much more dilute in the range of 5 or 10% catalyst can also be used satisfactorily.

Discovery of a suitable solvent for the metal lactam has also made possible the preparation of an active catalyst in liquid form which has good storage stability. Conventional synthesis of a liquid catalyst solution prior to this invention required the preparation of the metal lactam in excess lactam. Following reaction of metal and lactam, volatile reaction products were removed by dis tillation along with some lactam solvent. The lactam, having an elevated melting point, e.g. caprolactam melts at 69 0., solidified in the distillation lines unless the lines were heated and the distillation carried out at high temperature. The high temperature, combined with even trace amounts of water or carbon dioxide, resulted in gelation of the solution because of partial polymerization of the solution or in reduction of the catalytically active metal lactam to the catalytically inactive alkyl amine. Further, the catalyst solution after preparation had a relatively short shelf life range from a few hours to a few days and often had a reduced catalytic activity. The process of the present invention achieves in the prepared catalyst solution the paradoxical combination of both increased and decreased activity, regarding its catalytic effect and storage stability respectively. The process for preparing the lactam polymerization catalyst comprises reacting a metal hydride, metal hydroxide, metal alkyl, metal alkoxide, metal amide, metal carbonate, etc. with a lactam monomer in the presence of an N,N-disubstituted amine of the formula where R can be hydrogen or any monovalent hydrocarbon radical and where R and R can be any monovalent hydrocarbon radical and where any two of the Rs can be joined together to form a heterocyclic ring, followed by removal of volatile reaction products. One useful procedure has been to contact the metal with excess water or alcohol, and then to add the solvent and lactam monomer. The hydroxide or al'koxide group of the metal compound is displaced by the lactam. Reaction of the metal hydroxide or alkoxide with the lactam can be accelerated by application of heat to the mixture, after which time the alcohol or water is removed by distillation, optionally under reduced pressure. Alternatively, the catalyst solvent can be withheld until the reaction of metal compound and lactam is complete, after which time the solvent can be added and reaction products and excess reactants removed. To insure complete removal of all volatile materials, it is often desirable to continue the distillation until some portion of the solvent is also removed. As mentioned above, metal hydrides and metal alkyls can also be used in the instant process. The choice of which metal compound to react with a lactam will depend to some extent upon the reaction conditions. For instance, a magnesium alkyl can be added directly to a lactam monomer to form quickly the corresponding magnesium lactam. A magnesium alkoxide can be expected to react more slowly. An aluminum alkoxide, however, reacts so slowly that the use of an aluminum alkyl to form the aluminum lactam is definitely preferred. Similarly, the reaction of most metals other than the alkali metals, magnesium and aluminum with a lactam will benefit from the use of metal alkyl or hydrides to produce a satisfactory quantity of the metal lactam. Reaction temperatures can vary from room temperature or less up to 200 C. or more and pressures from subatmospheric to several hundred pounds per square inch. Reaction times can also vary considerably from a few seconds to several hours. If a metal alkyl or alkoxide is employed, the alkyl or alkoxy group can be of any size or degree of branching although relatively straight-chained groups having up to about 20 carbon atoms are preferred. Preferred reaction conditions for the alkali metal, magnesium and aluminum compounds 'with e-caprolactam are usually in the area of 50 to 150 C. at atmospheric pressures for from about minutes to an hour.

The third feature of the present invention is the improvement in base-catalyzed, substantially anhydrous lactam polymerizations made possible by the novel catalyst solutions described herein. In its broadest application, the improvement comprises dissolving a metal lactam polymerization catalyst in an N,N-disubstituted amide of the formula where R can be hydrogen or any monovalent hydrocarbon radical and where R and R can be any monovalent hydrocarbon radical and where any two of the Rs can be joined together to form a heterocyclic ring, prior to addition of said catalyst to said monomer. As recognized by many skilled artisans,

there are several acceptable lactam polymerization catalysts which need not be added to monomer in liquid form to produce an acceptable polymeric product. But many of the catalytic additives, such as sodium hydride, potassium hydride, magnesium methoxide, triethyl aluminum, ethyl magnesium bromide and methyl magnesium chloride react with monomeric lactam to give volatile reaction products such as hydrogen, ethane, methanol and ethanol. The volatile materials must be removed from the monomer prior to gelation to provide bubble-free products with uniform properties. Removal of the volatiles usually requires an evacuation step prior to polymerization which can consist of distillation under reduced pressure. If the monomer mixture is viscous because of partial polymerization or because of the large amount of additives such as inorganic reinforcing agent, the problem of volatiles removal is increased. If the catalytic precursors are prereacted with the monomer to form the active iminium salt in the absence of any initiator or other additives, the volatiles can be removed from the catalyst prior to its addition to the monomer. But metal lactams are solids and can only be dispersed with difficulty in a viscous monomer slurry. If dissolved in a small portion of monomer prior to addition to the monomer slurry, the catalyst can be dispersed if heated to 100 to 200 C. to keep it in liquid form. But at elevated temperatures, the catalyst is very susceptible to degradation or autocatalysis if trace amounts of water or carbon dioxide are present. The present invention obviates all the above difiiculties. It further provides a catalyst which produces cast polymers with good mechanical properties, an important feature of this invention.

One preferred process comprises a bulk or mass polymerization of a lactam by adding initiator, stabilizer, pigments, dyes, fillers, reinforcing agents or other additives to the molten monomer and mixing the catalyst solution of this invention With the monomer slurry as it is cast into heated molds. To shorten residence time in the molds, the initiated monomer slurry can also be preheated to an acceptable polymerization temperature before casting. Ample distribution of catalyst in the monomer can be assured by use of a mixing head. The other additives can be added in any order but efiicient dispersion of filler or reinforcing agent, if used, can be facilitated by adding them along 'with any dispersing aids first, followed by the initiator and then followed by the catalyst solution. As mentioned, the order of addition of the various additives to the lactam monomer can be altered in any manner desired. For instance, the catalyst solution and initiator can be added simultaneously to the monomer and filler subsequently added or the entire batch of ingredients can be mixed together at some reduced temperature of or C. and then heated rapidly to polymerization temperature and cast into molds. Other orders of addition are also included within the scope of the'present polymerization process.

Suitable monomers for use herein include those lactams of the following formula Where R is an alkylene group having from about 3 to about 12 carbon atoms. Preferred are the w-lactams where R is an unbranched group containing from about 5 to about 12 carbon atoms. A preferred monomer is e-caprolactam. Lactam monomers in addition to e-caprolactam include a-pyrrolidone, piperidone, valerolactam, caprolactams other than the e-isomer, methyl cyclohexanone isoximes, capryllactam, cyclodecanone isoxime and lauryllactam. Also included are mixtures of lactam monomers.

One important type of additive used in the practice of preferred embodiments of this invention are the fillers or reinforcing agents. As amply described in the now abancloned US. patent application Ser. No. 284,375, filed May 31, 1963, incorporated herein by reference, the incorporation of inorganic reinforcing agents into the polymerized product represents an important advance in the art. Although the present invention is quite useful in the production of unfilled polymeric shapes, it is particularly applicable in the manufacture of highly filled or reinforced polymers. This is so because of the increase in viscosity of a monomer slurry containing a solid phase and its consequent effect on thorough distribution of additives to the slurry. The term filler as used herein refers to any normally solid, non-polymerizable substance which can be dispersed in a polymer. Although fillers can vary in shape from granular through acicular to fibrous, dispersion in a polymer will require that the filler be small enough to be encapsulated by the polymer matrix forming the finished object. For most purposes, it is deirable that the filler have a water solubility of 0.15 gram per liter or less. Examples include materials selected from a wide variety of clays such as montrnorillonite, kaolinite, bentonite, hectorite, beidellite and attapulgite, other minerals and mineral salts such as chrysolite, alumina, saponite, hercynite, feldspar, quartz, wollastonite, mullite, kyanite, cristobalite, chrysotile, crocidolite, limestone, mica, spodumene and garnet, metals such as aluminum, tin, lead, magnesium, calcium, strontium, barium, titanium, zirconium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, metal oxides such as oxides of the foregoing metals, metal salts such as ferric phosphate, mercuric phosphate, lead phosphate, ferric aluminate and zinc aluminate, siliceous non-mineral substances such as precipitated calcium carbonate, silica gel, fume silica, glass fibers, fibrous aluminum silicate of the formula Al SiO and glass flakes, cellulosic materials such as wood chips, sawdust, wood flour, cotton fibers and cotton fioc, other organic materials such as thermosetting and other thermoplastic polymers in granular or fibrous form, and miscellaneous materials such as graphite whiskers, carbon filaments, silicon crystals, silicon carbide and the like.

Those fillers set forth above which have or can acquire hydroxyl groups attached to their surfaces can be converted into reinforcing adducts by reaction with a coupling agent. The term reinforcing adduct refers to the reaction product of a filler with a coupling agent. Fillers particularly preferred for conversion into reinforcing adducts are those siliceous materials characterized by a somewhat refractory nature with a melting point above 800 C., a Mohs hardness of at least 4, a water solubility of less than 0.1 gram per liter and a 3-dimensional crystal configuration as opposed to a 2-dimensional or planar crystal configuration possessed by some clays. Particularly preferred for use in the process of this invention are those fillers or reinforcing agents described above which have a length to diameter ratio (l/ d of about 25 to 1 or less. Quantities of reinforcing adduct, their sizes and shapes, types and quantities of coupler and methods of combination with fillers to form reinforcing adducts are amply described in copending US. patent application Ser. No. 413,456, filed Nov. 24, 1964, now US. Pat. No. 3,386,943, granted June 4, 1968, hereby incorporated by reference. Also described are a number of other additives and techniques which can be used herein to prepare a polymeric shape of high quality, cast directly from a monomer. Coupling agents referred to above are polyfunctional compounds having at least one functional group capable of reacting with hydroxyl groups and at least one functional group capable of chemically reacting with a polymerized polymer or polymerizing monomer. Particularly preferred coupling agents for use in the preparation of reinforced polyactams are those organosilanes having both alkoxy groups and lactam-reactive functional groups attached to the silicon atom. Examples of preferred couplers include l'IlCihYi-y-tlifllfithOXYSilYl propionate and 3-aminopropyltriethoxy silane.

The patent art contains several disclosures relating to base-catalyzed lactam polymerizations. Among them are US. 3,017,391, US. 3,017,392, US. 3,018,273, US. 3,028,369, US. 3,086,962 and US. 3,120,503. The above references disclose various initiators or promoters, regulators and reaction conditions for carrying out a basecatalyzed lactam polymerization. In general, the reaction components and reaction conditions described in the above patents are as equally suitable for the catalyst system described herein as they are for the catalyst systems set forth in the above patents.

The above invention will be more clearly understood in view of the following detailed examples. Quantities set forth below are expressed as parts or percent by weight unless otherwise stated.

EXAMPLE 1 To a solution of 10 grams of magnesium metal dissolved in 280 ml. of methanol is added 102 grams of caprolactam. Methanol is removed by distillation, after which time grams of N-methylpyrrolidone is added. Additional methanol is removed to leave a white precipitated residue. To the residue is added 37 grams of caprolactam and 30 grams N-methylpyrrolidone. Still further alcohol and some N-methylpyrrolidone are removed by distillation. The undistilled residue is in the form of a purple solution which is a viscous fluid at room temperature. Final weight of the solution which contains about 33% magnesium caprolactam, is 182 grams. Dilution of the solution with N-methylpyrrolidone to bring the magnesium caprolactam content down to 22% results in a clear purple non-viscous fluid at room temperature.

Storage of the solution for 30 days at room temperature results in no appreciable change nor does a 10 day storage at 110 C. produce any appreciable change.

EXAMPLE 2 To 97 grams of N-methylpyrrolidone is added 6 grams of sodium metal and 34 grams of caprolactam. The reactants are heated to 80 to 100 C. to produce a smooth reaction. Following completion of the reaction, the solution is refluxed for 15 minutes. The solution is poured into a bottle and becomes a solid at room temperature. The solution is fluid at 60 C. Storage of the solution at room temperature for 30 days or at C. for 10 days produces no appreciable change.

EXAMPLE 3 Example 2 is followed except that in place of the N- methylpyrrolidone, grams of N,N-dipropyl propionamide is used. The resultant solution is a clear liquid down to about 30 C. Whether stored at room temperature or at 110 C., the solution is stable.

EXAMPLE 4 To a solution of 10 grams of magnesium dissolved in 300 ml. of methanol is added 102 grams of caprolactam. Methanol is distilled from the mixture until a white pre cipitate forms. To the residue in the reaction vessel is added 100 grams of N,N-dimethyl acetamide and the distillation is continued. An additional 50 grams of dimethyl acetamide is added and the residual methanol removed. The residual solution is a clear non-viscous liquid at room temperature. The solution is stable at room temperature and at elevated temperature of 110 C.

EXAMPLE 5 Example 4 is repeated except that in place of the dimethyl acetamide is substituted an equal quantity of N,N- di nethyl formamide. The resultant solution is a clear semi-viscous liquid at room temperature and is stable both at room temperature and 110 C.

EXAMPLE 6 In this example the procedure described in Examples 4 and 5 above is repeated using instead of the solvent specitied in the above examples several other organic liquids chosen because of their potential utility as solvents for a metal lactam. The proposed solvents and the manner in which they perform are listed below:

Caprolactam produces a clear solution which slowly crystallized to form a solid not rendered liquid by subsequent heating.

Triamylamine produces a 2 phase mixture1 liquid and 1 solid.

Triethylenediamine produces a white precipitate.

N-ethylmorpholine produces a white precipitate.

Triphenylamine produces a White precipitate.

Phenylamine produces a white precipitate.

Naphthylamine produces a white precipitate.

Benzene produces a White precipitate.

Toluene produces a white precipitate.

Xylene produces a white precipitate.

Chlorobenzene produces a White precipitate.

p-Dichlorobenzene produces a white precipitate.

In general, with the exception of the caprolactam solvent, none of the foregoing organic liquids is capable of yielding a solution containing any appreciable amount of dissolved catalyst, either at room temperature or at 110 C. The solubility of catalyst in benzene and toluene at 110 C. was not ascertained because of their low boiling points at atmospheric pressure. Instead, an elevated temperature of 50 C. is employed. The catalyst is not soluble to any appreciable extent in either benzene or toluene at 50 C.

By comparison, the solvents included within the scope of the present invention produce clear solutions at the same temperatures.

EXAMPLE 7 To 3250 parts of micron anhydrous silica-having an average particle size of 2.1 microns is added 10 parts of 3-aminopropyl triethoxysilane. The two materials are dry blended for to minutes at 110 C., after which time the aggregates are redispersed by ball milling. To 2250 parts of molten e-caprolactam in an atmosphere of dry nitrogen is added the treated silica, 28 parts of an 80/20 mixture 2,4- and 2,6-toluene diisocyanate (TD80) and 0.2 part of triethylenediamine (Dabco). Also added is 28 parts (12 mmoles/mole) of magnesium bromide. The mixture is held at 120 C. and gaseous byproducts removed by stripping at a reduced pressure of about 6 mm. Hg. The stripping is continued until 500 parts of caprolactam are also removed. The vacuum is released and replaced by a nitrogen blanket. The slurry is heated to 175 C., and introduced into a mold through a mixing head which adds magnesium caprolactam dissolved in N- methylpyrrolidone. The catalyst solution is metered into the monomeric slurry at a rate which will provide 7 mmoles of magnesium caprolactam per mole of monomer. The mold is preheated to 175 C. and maintained at or near this temperature for 10 minutes after casting, after which time the monomeric slurry has solidified. Upon opening the mold, a smooth solid sheet having no voids or bubbles is revealed. The sheet is completely polymerized and mechanically isotropic.

EXAMPLE 8 The procedure described in Example 7 is followed except that no magnesium bromide is added to the monomer slurry and sodium caprolactam is used as the catalyst in place of the magnesium caprolactam. The sodium caprolactam is added to the monomer slurry in the form of a 33% solution in N-methylpyrrolidone. The polymeric sheet is similar in all respects to the polymerized sheet produced in Example 7.

10 EXAMPLE 9 To 2000 parts of molten s-caprolactam in an atmosphere of dry nitrogen is added 25 parts of an /20 mix ture of 2,4- and 2,6-toluene diisocyanate. The mixture is held at C., then heated to C. and cast into a mold through a mixing head which is used to meter a 33% solution of sodium caprolactam dissolved in N- methylpyrrolidone into the monomer. The catalyst solution is added in a quantity which provides 10 mmoles of sodium caprolactam per mole of monomer in the reactant mixture. The mold is preheated to 175 C. and maintained at or near this temperature for 5 minutes, after which time the material has solidified. Upon removal from the mold, the finished polymer is smooth, free from bubbles and voids and is completely polymerized.

What is claimed is:

1. In a base-catalyzed, substantially anhydrous anionic mass polymerization of a lactam employing a metal lactam catalyst and .a lactam polymerization initiator, the' improvement comprising dissolving said metal lactam in an N,N-disubstituted amide of the formula where R can be hydrogen or any monovalent hydrocarbon radical having up to about 20 carbon atoms, where R; and R can be any monovalent hydrocarbon radical having up to about 20 carbon atoms and where any two of the Rs can be joined together to form a heterocyclic ring having up to about 12 carbon atoms,

prior to adding said metal lactam to the monomeric lactam.

2. A process according to claim 1 wherein an inorganic filler material and a polymerization initiator are added to said monomeric lactam before said metal lactam is added to said monomeric lactam.

3. A process according to claim 1 wherein said metal lactam catalyst is sodium or magnesium caprolactam.

4. A process according to claim 1 wherein said N,N- disubstituted amide is a liquid at 40 C.

5. A process according to claim 1 wherein said N,N- disubstituted amide is N-methylpyrrolidone.

6. A process according to claim 1 wherein the solution formed by dissolving said metal lactam in said N,N-disubstituted amide contains at least 25% by weight metal lactam.

7. A process according to claim 6 wherein said solution contains at least 50% by weight metal lactam.

8. A process according to claim 1 wherein said monomeric lactam is an w-lactam.

9. A process according to claim 8 wherein said monomeric lactam is e-caprolactam.

References Cited UNITED STATES PATENTS 3,211,706 10/1965 Borner 26078 3,359,227 12/1967 Amann et a1. 26030.8 3,360,503 12/ 1967 Bantjes 260-78 3,417,163 12/1968 Beermann et al 260857 3,451,963 6/1969 Tierney et a1. 26037 3,488,319 1/1970 Miller 26078LX WILLIAM H. SHORT, Primary Examiner L. M. PHYNES, Assistant Examiner U.S. Cl. X.R. 26037 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3, 575, 938 Dated April 20, 1971 Inventor-(e) Paul A. Tierney It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:

Column 1, line 55, in the formula the bond from R to C (second occurrei is omitted. See specification, page 1.

Column 3, line 5, "detail' should read detailed See specification, page 3, line 19.

Column 3, line 73, "condenser" should read condensed See specification, page 5, line 4.

Column 4, line 50, "temperatures" should read temperature See specification, page 6, line 10.

Column 4, line 70, "range" should read ranging See specification, page 6, line 25.

Column 5, line 4, "amine" should read amide See specification, page 6, line 32.

Column 6, line 2, "added to monomer in liquid" should read added 1::

the monomer in liquid See specification, page 8, line 15.

Column 7, line 18, "deirable" should read desirable See specification, page 10, line 16.

Signed and sealed this 13th day of. August 1974.

(SEAL) Attest:

MCCOY M. GIBSON, JR. C. MARSHALL DANN Attesting Officer Commissioner of Patent 

